Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F20/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
  • C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
  • C08F220/04—Acids; Metal salts or ammonium salts thereof

Definitions

• This invention relates to an interpolymer of olefinically unsaturated carboxylic acids or anhydrides and a polymeric surface active agent (or surfactant), having a linear block or random comb configuration which provides a steric stabilizing component to the interpolymer and produces a polymer which is easier to disperse and handle.
• Such polymers may be homopolymers of unsaturated polymerizable carboxylic acids, such as acrylic acid, methacrylic acid, maleic acid, maleic anhydride, itaconic acid and the like; or copolymers of said acid or anhydride monomers with (meth)acrylate esters, (meth)acrylamides, olefins, maleic anhydrides, vinyl esters, vinyl ethers, and styrenics; or copolymers with other vinyl or vinylidene monomers.
• copolymers of these acids are cross-linked with small amounts of cross-linking agents.
• Surfactants have been employed in the manufacture of carboxyl containing polymers because, in their manufacture, the aggregation of the polymer can interfere with the polymerization reaction by retarding access of the monomer to free radicals and by interfering with the removal of the heat produced by the polymerization. Further, the precipitated polymer forms a slurry in the solvent which becomes extremely thick, resulting in ineffective mixing and fouling on reactor surfaces. In response to these problems, and to increase the usually low total solids to a range of about 8 to 17 weight percent and increase productivity, a variety of surfactants have been employed.
• U.S.-A-4,375,533 to Park et al. discloses a process for overcoming some of the above problems, in which the polymerization of acrylic acid, and optional comonomers, in an organic media, is characterized by the use of nonionic surface active agents having a hydrophobe to lipophobe balance (HLB) values between 1 and about 10.
• HLB hydrophobe to lipophobe balance
• U.S.-A-4,420,596, to Lochhead et al. disclosed a process for polymerizing carboxylic acids in mineral spirits, employing nonionic surface active agents having HLB values less than 10.
• U.S.-A-4,526,937 to Hsu teaches the polymerization of acrylic acid in an organic solvent with a free radical catalyst, using nonionic block copolymers of propylene oxide and ethylene oxide to minimize undesirable flocculation and agglomeration.
• FR-A-2 270 268 discloses a method for the polymerization of vinyl monomers selected from substituted or unsubstituted styrene, (meth)acrylates, vinylacetates, acrylonitrile or vinylchloride in the presence of a block copolymer of the AB-type, wherein A is the lipophilic and B is the hydrophilic block of the polymer.
• the present invention resulted from the discovery that in polymerizing olefinically unsaturated carboxylic acid or anhydride monomers containing at least one activated carbon to carbon olefinic double bond and at least one carboxyl group, in an organic media, in the presence of free radical forming catalysts and at least one steric stabilizing polymeric surface active agent (also called surfactant), having at least one hydrophilic moiety and at least one hydrophobic moiety and a linear block or random comb configuration, or mixtures thereof or with other surfactants, an interpolymer, useful as a thickening and emulsifying agent, is produced which is easier to handle and to disperse.
• the carboxylic acid or anhydride will be at least 15% by weight of the interpolymer.
• the steric stabilizing surfactant appears to become a part of the polymer molecule by a bonding mechanism or by becoming entangled in the polymer as in an interpenetrating network or by some other force which seems to keep it associated with the polymer molecule.
• the steric stabilizing surfactant is a molecule of surfactant that has a hydrophilic portion which is associated with the polymer and a hydrophobic portion which extends from the polymer to provide steric stability.
• the resultant polymer possesses unexpectedly better handling and dispersing characteristics, as well as increased thickening efficiency at lower cross linker concentrations.
• one is able to obtain an improved interpolymer which is easy to disperse and to handle, and yields lower dispersion viscosities, combined with favorable final application properties such as increased thickening efficiency.
• This product is achieved using a steric stabilizing surfactant (or steric stabilizer) which becomes associated with the resin in the final product as an interpolymer.
• the present invention invention relates to the interpolymer of claim 1 and the method of making said interpolymer of claim 18. Preferred embodiments are apparent from the dependent claims.
• the steric stabilizer may also be used in combination with other surfactants.
• the amount of steric stabilizing surfactant used in an amount of between 0.01 to 10% is preferred, and 0.2 to 6.0% is further preferred, based upon the weight of the olefinically unsaturated carboxylic acids or anhydrides, to be polymerized.
• the carboxylic acid or anhydride preferably comprises at least 40% by weight of the interpolymer.
• Polymerization of the carboxyl-containing monomers, optionally with other vinylidene comonomers, is usually carried out in the presence of a free radical catalyst in a closed vessel in an inert atmosphere under autogenous or artificially-induced pressure, or in an open vessel in an inert atmosphere optionally under reflux at atmospheric pressure.
• the temperature of the polymerization may be varied from 0° to 125° C or lower or higher.
• Polymerization at 25° to 90°C using a free radical catalyst is generally effective in providing monomer to polymer conversions of 75 percent to 100 percent.
• the polymerizations may be either batch, semi-batch or continuous.
• the agitation may be any agitation sufficient to maintain the slurry and obtain effective heat transfer including, for example, helical agitation, pitched turbines and the like.
• a useful reaction temperature range is from the range of 20° C to 90° C at 101.3 kPa (1 atmosphere) or more Normal polymerization time is from to 12 hours.
• Typical free-radical forming catalysts include peroxygen compounds such as sodium, potassium and ammonium persulfates, caprylyl peroxide, benzoyl peroxide, hydrogen peroxide, pelargonyl peroxide, cumene hydroperoxides, diisopropyl peroxydicarbonate, tertiary butyl diperphthalate, tertiary butyl perbenzoate, sodium peracetate and di-(2-ethylhexyl) peroxy dicarbonate, as well as azo catalysts such as azobis(isobutyronitrile).
• Other catalysts utilizable are the so-called "redox' type of catalyst and the heavy-metal activated catalyst systems.
• Ultraviolet light may also be used to generate free radicals. Some systems polymerize solely by heat, but catalysts generally provide better control. The monomers may be batch charged or continuously added during the course of polymerization or by any other manner of polymerization techniques conventionally used.
• the medium used for the polymerization is an organic fluid, or mixtures of organic fluids, in which the monomers are preferably soluble but in which the polymer is substantially insoluble, so that the polymer product is preferably obtained as a fine friable or fluffy precipitate.
• the organic media is selected from the group consisting of hydrocarbons containing 6 to 40 carbon atoms, halocarbons, chlorofluoroalkanes, esters, and ketones.
• Typical monomer solvents include liquid hydrocarbons selected from alkanes of 5 to 10, preferably 6 to 8 carbon atoms, such as hexane and heptane; cycloalkanes of 4 to 8, preferably 5 to 7 carbon atoms, such as cyclohexane; benzene and alkyl-substituted benzenes containing 1 to 2 lower alkyl substituents, preferably methyl substituents, such as toluene and xylene; alkyl carboxylates containing 1 to 6 preferably 1 to 4 carbon atoms in the alkyl groups and 2 to 6, preferably 2 to 4 carbon atoms in the carboxylate moiety, such as ethyl acetate, isopropyl acetate, propyl acetate, methyl acetate, and butyl acetate; haloalkanes and chlorofluoroalkanes, containing 1 to 3 carbon atoms and at least 2 halo groups,
• Such polymers are homopolymers of an unsaturated, polymerizable carboxylic monomers such as acrylic acid, methacrylic acid, maleic acid, itaconic acid and maleic anhydride, and copolymers of polymerizable carboxylic monomers with acrylate esters, acrylamides, olefins, vinyl esters, vinyl ethers, or styrenics.
• the carboxyl containing polymers have molecular weights greater than 500 to as high as several million, usually greater than 10,000 to 900,000 or more.
• Copolymers include copolymers of acrylic acid with small amounts of polyalkenyl polyether cross-linkers that are gel-like polymers, which, especially in the form of their safts, absorb large quantities of water or solvents with subsequent substantial increase in volume.
• Carboxylic polymers and copolymers such as those of acrylic acid and methacrylic acid also may be cross-linked with polyfunctional materials as divinyl benzene and unsaturated diesters as is disclosed in U.S. -A-2,340,110 ; 2,340,111 ; and 2,533,635 .
• Olefinically-unsaturated acids of this class include such materials as the acrylic acids typified by the acrylic acid itself, alpha-cyano acrylic acid, beta methylacrylic acid (crotonic acid), alpha-phenyl acrylic acid, beta-acryloxy propionic acid, cinnamic acid, p-chloro cinnamic acid, 1-carboxy-4-phenyl butadiene-1,3, itaconic acid, citraconic acid, mesaconic acid, glutaconic acid, aconitic acid, maleic acid, fumaric acid, and tricarboxy eth lene.
• acrylic acids typified by the acrylic acid itself, alpha-cyano acrylic acid, beta methylacrylic acid (crotonic acid), alpha-phenyl acrylic acid, beta-acryloxy propionic acid, cinnamic acid, p-chloro cinnamic acid, 1-carboxy-4-phenyl butadiene-1,3, itaconic acid, cit
• carboxylic acid includes the polycarboxylic acids and those acid anhydrides, such as maleic anhydride, wherein the anhydride group is formed by the elimination of one molecule of water from two carboxyl groups located on the same carboxylic acid molecule.
• R and R' are selected from the group consisting of hydrogen, halogen and cyanogen (-C ⁇ N) groups and alkyl, aryl, alkaryl, aralkyl, and cycloalkyl groups such as methyl, ethyl, propyl, octyl, decyl, phenyl, tolyl, xylyl, benzyl and cyclohexyl.
• the preferred carboxylic monomers are the monoolefinic acrylic acids having the general structure wherein R 2 is a substituent selected from the class consisting of hydrogen, halogen, and the cyanogen (-C ⁇ N) groups, monovalent alkyl radicals, monovalent aryl radicals, monovalent aralkyl radicals, monovalent alkaryl radicals and monovalent cycloaliphatic radicals. Of this class, acrylic and methacrylic acid are most preferred. Other useful carboxylic monomers are maleic acid and its anhydride.
• the polymers include both homopolymers of carboxylic acids or anhydrides thereof, or the defined carboxylic acids copolymerized with one or more other vinylidene monomers containing at least one terminal >CH 2 group.
• the other vinylidene monomers are present in an amount of less than 30 weight percent based upon the weight of the carboxylic acid or anhydride plus the vinylidene monomer(s).
• Such monomers include, for example, acrylate ester monomers including those acrylic acid ester monomers such as derivatives of an acrylic acid represented by the formula wherein R 3 is an alkyl group having from 1 to 30 carbon atoms, preferably 1 to 20 carbon atoms and R 2 is hydrogen, methyl or ethyl, present in the copolymer in amount, for example, from 1 to 40 weight percent or more.
• acrylate ester monomers including those acrylic acid ester monomers such as derivatives of an acrylic acid represented by the formula wherein R 3 is an alkyl group having from 1 to 30 carbon atoms, preferably 1 to 20 carbon atoms and R 2 is hydrogen, methyl or ethyl, present in the copolymer in amount, for example, from 1 to 40 weight percent or more.
• acrylates include methyl acrylate, ethyl acrylate, propyl acrylate, isopropyl acrylate, butyl acrylate, isobutyl acrylate, methyl methacrylate, methyl ethacrylate, ethyl methacrylate, octyl acrylate, heptyl acrylate, octyl methacrylate, isopropyl methacrylate, 2-ethylhexyl methacrylate, nonyl acrylate, hexyl acrylate and n-hexyl methacrylate.
• Higher alkyl acrylic esters are decyl acrylate, isodecyl methacrylate, lauryl acrylate, stearyl acrylate, behenyl acrylate and melissyl acrylate. Mixtures of two or three or more long chain acrylic esters may be successfully polymerized with one of the carboxylic monomers.
• Other comonomers include olefins, including alpha olefins, vinyl ethers, vinyl esters, and mixtures thereof.
• Cross-linking monomers for use in preparing the copolymers are polyalkenyl polyethers having more than one alkenyl ether grouping per molecule. They are made by the etherification of a polyhydric alcohol containing at least 2 carbon atoms and at least 2 hydroxyl groups. Compounds of this class may be produced by reacting an alkenyl halide, such as allyl chloride or allyl bromide, with a strongly alkaline aqueous solution of one or more polyhydric alcohols. The product may be a complex mixture of polyethers with varying numbers of ether groups. Analysis reveals the average number of ether groupings on each molecule.
• Efficiency of the polyether cross-linking agent increases with the number of potentially polymerizable groups on the molecule. It is preferred to utilize polyethers containing an average of two or more alkenyl ether groupings per molecule. Typical agents are allyl pentaerythritol, allyl sucrose, and trimethylolpropane diallyl ether.
• the polymeric mixtures contain 0.01 to 5% by weight of cross-linking monomer based on the total of carboxylic acid monomer, plus other monomers, if present, and more preferably 0.01 to 3.0 weight percent.
• vinylidene monomers may also be used, including the acrylic nitrites.
• the useful ⁇ , ⁇ -olefinically unsaturated nitriles are preferably the monoolefinically unsaturated nitriles having from 3 to 10 carbon atoms such as acrylonitrile and methacrylonitrile. Most preferred are acrylonitrile and methacrylonitrile.
• the amounts used are, for example, for some polymers are from 1 to 30 weight percent of the total monomers copolymerized.
• Acrylic amides containing from 3 to 35 carbon atoms including monoolefinically unsaturated amides also may be used.
• amides include acrylamide, methacrylamide, N-t-butyl acrylamide, N-cyclohexyl acrylamide, higher alkyl amides, where the alkyl group on the nitrogen contains from 8 to 32 carbon atoms, acrylic amides including N-alkylol amides of alpha,beta-olefinically unsaturated carboxylic acids including those having from 4 to 10 carbon atoms such as N-methylol acrylamide, N-propanol acrylamide, N-methylol methacrylamide, N-methylol maleimide, N-methylol maleamic acid esters and N-methylol-p-vinyl benzamide.
• Still further useful materials are alpha-olefins containing from 2 to 30 carbon atoms, preferably 2 to 18 and more preferably from 2 to 8 carbon atoms; dienes containing from 4 to 10 carbon atoms; vinyl esters and allyl esters such as vinyl acetate; vinyl aromatics such as styrene, methyl styrene and chlorostyrene; C 1 -C 5 alkyl vinyl ethers and allyl ethers and ketones such as vinyl methyl ether and methyl vinyl ketone; chloroacrylates; cyanoalkyl acrylates such as ⁇ -cyanomethyl acrylate, and the ⁇ -, ⁇ -, and ⁇ -yanopropyl acrylates; alkoxyacrylates such as methoxy ethyl acrylate; haloacrylates as chloroethyl acrylate; vinyl halides and vinyl chloride and vinylidene chloride; divinyls, diacrylates and other polyfunctional monomers such as divin
• the steric stabilizer functions to provide a steric barrier which repulses approaching particles.
• a requirement for the steric stabilizer is that a segment of the dispersant (i.e., a hydrophobe) be very soluble in the solvent (the continuous phase in a nonaqueous dispersion polymerization process) and that another segment (i.e., a hydrophile) be at least strongly adhered to the growing polymer particle.
• the steric stabilizers of the present invention have a hydrophilic group and a hydrophobic group.
• the steric stabilizers are block copolymers comprising a soluble block and an anchor block having a molecular weight (i,e., chain length) usually well above 1000, but a hydrophobe length of more than 5 nm (50 Angstroms), as calculated by the Law of Cosines. These dimensions are determined on the extended configuration using literature values for bond lengths and angles.
• the steric stabilizers of the present invention are distinguishable from the prior art steric surfactants which may be block copolymers, but have hydrophobe lengths of less than 5 nm (50 Angstroms).
• the steric stabilizer of the present invention has either a linear block or a comb configuration, and has a hydrophobe of sufficient length to provide a sufficient steric barrier.
• the steric stabilizer is a linear block copolymeric steric stabilizer, it is defined as mentioned above.
• hydrophilic groups are polyethylene oxide, poly(1,3-dioxolane), copolymers of polyethylene oxide or poly(1,3-dioxolane), poly(2-methyl-2-oxazoline polyglycidyl trimethyl ammonium chloride and polymethylene oxide, with polyethylene oxide being preferred.
• hydrophobic groups are polyesters, such as those derived from 2-hydroxybutyric acid, 3-hydroxybutyric acid, 4-hydroxybutyric acid, 2-hydroxycaproic acid, 10-hydroxydecanoic acid, 12-hydroxydodecanoic acid, 16-hydroxyhexadecanoic acid, 2-hydroxyisobutyric acid, 2-(4-hydroxyphenoxy) propionic acid, 4-hydroxyphenylpyruvic acid, 12-hydroxystearic acid, 2-hydroxyvaleric acid, polylactones, such as caprolactone, butyrolactone, polylactams, such as those derived from caprolactam, polyurethanes, polyisobutylene, where the hydrophobe should provide a steric barrier of greater than 5 nm (50 Angstoms), preferably greater than 7.5 nm (75 Angstroms), with greater than 10 nm (100 Angstroms) being also preferred, with polyhydroxy fatty acids, such as poly(12-hydroxystearic acid) being preferred.
• the steric barrier
• Steric stabilizer molecules comprise both hydrophilic and hydrophobic units.
• Hydrophobic polymer units or hydrophobic blocks may be prepared by a number of well known methods. These methods include condensation reactions of hydroxy acids, condensation of polyols (preferably diols) with polycarboxylic acids (preferably diacids).Other useful methods include polymerization of lactones and lactams, and reactions of polyols with polyisocyanates. Hydrophobic blocks or polymer units can be reacted with hydrophilic units by such reactions as are known to those skilled in the art. These reactions include condensation reactions and coupling reactions, for example. Subsequent to the steric stabilizer preparation, the stabilizers may be further reacted with modifying agents to enhance their utility. U.S.-A-4,203,877 to Alan S. Baker teaches making such steric stabilizers, and the entire disclosure thereof is incorporated herein by reference.
• the steric stabilizer is a random copolymeric comb steric stabilizer, it is defined as mentioned above.
• hydrophobic monomer unit or moiety examples include dimethyl siloxane, diphenyl siloxane, methylphenyl siloxane, alkyl acrylate and alkyl methacrylate, with dimethyl siloxane being preferred.
• hydrophilic monomer unit or moiety examples include methyl-3-polyethoxypropyl siloxane-n-phosphate or sulfate, and the alkali metal or ammonium salts derived therefrom; units derived from polyethoxy (meth)acrylate containing from 1 to 40 moles of ethylene oxide; acrylic acid; acrylamide-, methacrylic acid, maleic anhydride; dimethyl amino ethyl (meth)acrylate; or its salts with methyl chloride or dimethyl sulfate; dimethyl amino propyl(meth)acrylamide and its salts with methyl chloride or dimethyl sulfate, with methyl-3-polyethoxypropyl siloxane- ⁇ -phosphate being preferred.
• terminating agents are monohalo silanes, mercaptans, haloalkanes, alkyl aromatics and alcohols, which will produce terminating groups such as trialkyl silyl, alkyl, aryl alkyl and alcoholate, with the preferred terminating groups being trimethyl silyl.
• a random copolymeric comb steric stabilizer is a dimethicone copolyol phosphate which has the following formula: where x and y are integers greater than 1, and z is an integer from 1 to 100.
• Such a copolymeric comb steric stabilizer is available commercially under the trade name Pecosil® from Phoenix Chemical, Somerville, New Jersey
• the steric stabilizers of the appropriate structure in accordance with the present invention have the potential for becoming part of a (meth)acrylic acid or anhydride-containing polymer as an interpolymer by several mechanisms, including a bonding mechanism. These would include graft-type polymerization, hydrogen bonding, olefinic unsaturation polymerization, or condensation reaction. While we do not wish to be bound by a particular bonding mechanism theory, its explanation is felt to be helpful in understanding the invention.
• the polyethylene oxide segment which is known to hydrogen bond strongly to polycarboxylic acids, will react with the polycarboxylic acid and result in the formation of a hydrogen bonded complex.
• longer polyethylene oxide segments will give more strongly-bonded complexes.
• Another possible bonding mechanism is the polymerization of olefinic unsaturation in the stabilizer with the growing polymer chain.
• Some stabilizers contain a certain degree of unsaturation and this unsaturation may react via the following general pathway:
• a polymerization reaction was conducted in a water jacketed two liter Pyrex resin kettle equipped with mechanical stirrer, a thermometer and reflux condenser topped with a nitrogen inlet connected to a bubbler to provide a slightly positive pressure of nitrogen throughout the polymerization.
• the water jacket was connected to a constant temperature circulator.
• the resin kettle was charged with ethyl acetate (688.5 grams), cyclohexane (586.5 grams), acrylic acid (218.25 grams), stearyl methacrylate (6.75 grams), allylpentaerythritol (1.35 grams), and a steric stabilizing surface active agent in accordance with the present invention in a varied amount based upon the weight of the acrylic acid and co-acrylate ester monomers (i.e., phm or parts per hundred monomers).
• AA interpolymer In making an acrylic acid interpolymer (hereinafter also referred to as AA interpolymer), no stearyl methacrylate was used, the amount of acrylic acid was 225 grams, the amount of allylpentaerythritol was 2.25 grams, and the amount of steric stabilizer was based upon the amount of acrylic acid monomer solids. In either case, the mixture was sparged with nitrogen for 30 minutes while the reactor was heated to 50°C, At 50°C, the sparging tube was removed while a nitrogen purge was maintained, stirring was begun, and the recipe amount of di-(2-ethylhexyl)-peroxydicarbonate (in an amount of 0.275 to 0.98 grams) was added.
• Dispersion times were done using a 1% dispersion (4 g resin/396 g water) prepared in demineralized (DM) water, using a Servodyne mixer (Cole Parmer) with an S-paddle at 400 rpm.
• the resin was introduced through a 0.84 mm (20 mesh) screen, with stirring.
• the speed of hydration was visually assessed by the transparency of the wetted swollen microgels. The more transparent the microgel particle appears to be, the faster is the speed of hydration.
• the powder was considered not to be “easy to disperse”. Typically, if the product was dusty, i.e., fine, it was also not was easy to disperse.
• a clarity measurement is the percentage of light transmitted through the dispersed, hydrated and neutralized polymer at a resin concentration of 0.5%. Clarity is measured with a Brinkman PC 801 colorimeter at 420 nanometers (nm). The higher the percent transmittance, the better the clarity A transmittance of greater than 60% is acceptable.
• a 1% stock dispersion of resin or interpolymer (8 g resin/792 g water) was prepared in demineralized (DM) water, using a Lightnin' mixer at 1,000 rpm with a 3-blade marine impeller. The resin was introduced through a 0.84mm (20 mesh) screen with stirring and the dispersion was mixed for a total of one hour.
• the viscosity of the dispersion is referred to as the Dispersion Viscosity or Un-neutralized Viscosity.
• Dispersions can also be made with 2.5% resin, in which case the amounts are adjusted proportionately.
• An easy to disperse and easy to handle polymer will have a low dispersion time, in terms of minutes to disperse, while also having a relatively low dispersion (i.e., Un-neutralized) Viscosity.
• Un-neutralized dispersion Viscosity
• resin at 1 % resin an Un-neutralized Dispersion Viscosity of less than 1000 mPa ⁇ s [centipoise (cPs)] would be desirable, while at 2.5% resin an Un-neutralized Viscosity of less than 6000 mPa ⁇ s (cPs) is desirable.
• the 1% stock dispersion was then used to make the following typical concentrations for analysis, some or all of which may be measured: 0.2% Mucilage (80 g of stock dispersion diluted to a total of 400 g with DM water) 0.5% Mucilage (200 g of stock dispersion diluted to a total of 400 g with DM water) 1.0% Mucilage (400 g of stock dispersion used as is)
• the samples were then measured for pH and Brookfield Viscosity using a Brookfield RVT-DV Viscometer at 20 rpm.
• the viscosity of the neutralized dispersions is referred to as the Neutralized Viscosity.
• a Neutralized Viscosity of more than 20,000 mPa ⁇ s (cPs) at 0.5% resin concentration is desirable.
• Salt sensitivity on 1.0% mucilages are evaluated at 1.0% salt concentrations in the following manner:
• an interpolymer made from comonomers, incorporating a steric stabilizer in accordance with the present invention, is easier to disperse while retaining good ultimate thickening properties.
• the dispersion times for the Un-neutralized Dispersions are less than 15 minutes when compared to 75 minutes for the control resin (i.e., no steric stabilizer), and the interpolymers generally achieve less than 1000 mPa ⁇ s (cPs) un-neutralized viscosities.
• the neutralized resins have viscosities of greater than 20,000 mPa ⁇ s (cPs), and the interpolymers show good salt sensitivity.
• interpolymers can be produced under varying amounts of steric stabilizer and/or varying amounts of crosslinker
• polymers were prepared in accordance with the typical co-interpolymer reaction, using Hypermer® B-239 surfactant as the steric stabilizer.
• the amount of crosslinker i.e., allylpentaerythritol
• the steric stabilizer was varied in an amount of between 0.25% and 5.0% by weight based upon the weight of the monomer (parts per hundred weight of monomer or phm) while the amount of crosslinker was held constant (Examples 18-25).
• the polymerization solids, the vinylic monomers, i.e., the amount of acrylic acid plus co-acrylate ester monomer solids was 15% by weight based upon the total weight of the vinylic monomers plus the polymerization solvent.
• Crosslinker Steric Stabilizer dose Neutralized Viscosity 1% Salt Sensitivity Viscosity (mPa ⁇ s) (phm) (phm) (mPa ⁇ s) 1.0% Resin 12 0.2 1.0 4,020 7,600 13 0.4 1.0 11,400 7,800 14 0.6 1.0 31,000 8,250 15 0.8 1.0 67,000 7,450 16 1.0 1.0 109,000 5,200 17 1.2 1.0 137,000 3,300 18 0.6 0.25 34,600 7,900 19 0.6 0.50 38,000 8,650 20 0.6 0.75 34,800 8,200 21 0.6 1.0 31,000 8,250 22 0.6 1.5 36,000 7,950 23 0.6 2.0 39,200 7,700 24 0.6 3.0 43,400 7,250 25 0.6 5.0 50,000 6,850
• the samples consist of a control (i.e., without steric stabilizing surfactant), along with the four samples prepared with 5% by weight, based upon the weight of the acrylic acid monomers, of a steric stabilizer, namely, Hypermer® B-239, B-246, or B-261 surfactant, added to the monomer premix prior to initiation of the polymerization and a "post-add" control sample in which a control sample was reslurried in cosolvent and 5% steric stabilizer (Hypermer® B-261 surfactant) was added (i.e., post added) to the slurry which was then dried.
• a control i.e., without steric stabilizing surfactant
• a steric stabilizer namely, Hypermer® B-239, B-246, or B-261 surfactant
• the use of a steric stabilizer has little effect on weight average molecular weight (Mw) of the polymer.
• Mw weight average molecular weight
• the ability to extract the steric stabilizer decreases as the molecular weight of the steric stabilizer increases, presumably due to interpolymer chain entanglements.
• This can be corroborated by the fact that it is possible to extract nearly twice as much of the Hypermer® B-261 surfactant out of the post added sample of polyacrylic acid as in the pretreatment case.
• the fact that not all the Hypermer® B-261 surfactant in the post add case is extractable is explained by the high affinity for hydrogen bonding between the polyethylene oxide blocks in the steric stabilizers and the carboxylic acids on the surface of the resin particles.
• the strength of the hydrogen bonded complex will be related to the relative length of the polyethylene oxide block, the greater the number of hydrogen bonded sites, the stronger the complex.
• the molecular weight data on the steric stabilizers also substantiates the molecular weight dependency on extractability.
• the molecular weight data is very close between the pure and extracted samples, indicating a uniform extraction.
• the extracted molecular weight is significantly lower than the pure material, with the Hypermer® B-261 surfactant being the lowest. This shows a definite bias for the extractability of the low molecular weight fractions in the steric stabilizers.
• Vazo® 67 which is azobis(2-methyl butyronitrile), and available from the E.I. du Pont de Nemours & Company, Inc. was substituted for the di-(2-ethylhexyl)-peroxydicarbonate used in the typical copolymer reaction and an inter-polymer was produced that had a neutralized viscosity of 80,000 mPa ⁇ s (cPs) at 1.0% resin concentration and a clarity of 89%, which are desirable end thickening properties.
• cPs mPa ⁇ s
• cyclohexane was employed as the solvent in accordance with the typical co-interpolymer reaction, at crosslinker levels of 0.6 and 0.8 parts per hundred vinylic monomer (phm) and 12% total solids using Hypermer® 2234 surfactant at a dose of 4.0 phm, and an interpolymer was produced which achieved dispersion viscosities of 320 and 15 mPa ⁇ s (cPs) at 2.5% resin concentration, 11,000 and 37,000 mPa ⁇ s (cPs) neutralized viscosity at 0.5% resin concentration, and clarity of 88 and 48%, respectively.
• Example A was repeated using a different cut of mineral spirits, namely, one having a flash point of 79.4°C (175°F)
• the resulting polymer at a 0.5% mucilage, had a neutralized viscosity of 43,500 mPa ⁇ s (cPs) which demonstrates that the same results can be achieved using different solvents.
• the reaction mixture was sparged with dry nitrogen for 15 minutes at room temperature and then the reaction mixture was heated to 72°C with sparging for an additional 15 minutes.
• PEG polyethylene glycol
• PEG ethers Brij® brand surfactants
• Triton® brand surfactants PEG diesters
• PEG polysorbate esters Teween surfactants
• fatty acid partial esters of sorbitan Span® surfactants
• ethylene oxide block copolymers Pluronic® brand surfactants
• this invention claims an interpolymer which by utilizing a steric stabilizing surfactant in the polymerization of the resin is easy to disperse and/or has increased efficiency. These resins disperse in minutes when added to water, yield lower un-neutralized dispersion viscosities and have no detrimental effects on final application properties.

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• 1992
  • 1992-08-26 US US07/935,616 patent/US5288814A/en not_active Expired - Lifetime
• 1993
  • 1993-08-03 AU AU44388/93A patent/AU676841B2/en not_active Ceased
  • 1993-08-18 IL IL10672493A patent/IL106724A/en not_active IP Right Cessation
  • 1993-08-20 TW TW82106718A patent/TW260676B/zh not_active IP Right Cessation
  • 1993-08-20 MY MYPI93001658A patent/MY110032A/en unknown
  • 1993-08-20 BR BR9303434A patent/BR9303434A/pt not_active IP Right Cessation
  • 1993-08-20 MY MYPI97001605A patent/MY132334A/en unknown
  • 1993-08-23 ZA ZA936157A patent/ZA936157B/xx unknown
  • 1993-08-24 EP EP93113458A patent/EP0584771B2/en not_active Expired - Lifetime
  • 1993-08-24 ES ES93113458T patent/ES2111673T5/es not_active Expired - Lifetime
  • 1993-08-24 AT AT93113458T patent/ATE161553T1/de not_active IP Right Cessation
  • 1993-08-24 DE DE69315910T patent/DE69315910T2/de not_active Expired - Lifetime
  • 1993-08-24 MX MX9305127A patent/MX183685B/es unknown
  • 1993-08-25 CA CA002104835A patent/CA2104835A1/en not_active Abandoned
  • 1993-08-25 CN CN93116799A patent/CN1051094C/zh not_active Expired - Lifetime
  • 1993-08-26 KR KR1019930016896A patent/KR100294936B1/ko not_active IP Right Cessation
  • 1993-08-26 JP JP21157193A patent/JP3273089B2/ja not_active Expired - Lifetime
  • 1993-11-23 US US08/156,158 patent/US5349030A/en not_active Expired - Lifetime
• 1994
  • 1994-02-17 US US08/198,007 patent/US5373044A/en not_active Expired - Lifetime
  • 1994-11-29 US US08/346,121 patent/US5468797A/en not_active Expired - Lifetime

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